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EP0768333B1 - Procédé pour la fabrication de particules de résine thermodurcissables - Google Patents

Procédé pour la fabrication de particules de résine thermodurcissables Download PDF

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Publication number
EP0768333B1
EP0768333B1 EP95119961A EP95119961A EP0768333B1 EP 0768333 B1 EP0768333 B1 EP 0768333B1 EP 95119961 A EP95119961 A EP 95119961A EP 95119961 A EP95119961 A EP 95119961A EP 0768333 B1 EP0768333 B1 EP 0768333B1
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EP
European Patent Office
Prior art keywords
particles
water
cloud point
particle size
suspension
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
EP95119961A
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German (de)
English (en)
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EP0768333A2 (fr
EP0768333A3 (fr
Inventor
Haruhiko Sato
Yutaka Harada
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nippon Paint Co Ltd
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Nippon Paint Co Ltd
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Publication date
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Publication of EP0768333A3 publication Critical patent/EP0768333A3/fr
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Classifications

    • G—PHYSICS
    • G03—PHOTOGRAPHY; CINEMATOGRAPHY; ANALOGOUS TECHNIQUES USING WAVES OTHER THAN OPTICAL WAVES; ELECTROGRAPHY; HOLOGRAPHY
    • G03G—ELECTROGRAPHY; ELECTROPHOTOGRAPHY; MAGNETOGRAPHY
    • G03G9/00—Developers
    • G03G9/08—Developers with toner particles
    • G03G9/087—Binders for toner particles
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F6/00—Post-polymerisation treatments
    • C08F6/14—Treatment of polymer emulsions
    • C08F6/18—Increasing the size of the dispersed particles
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J3/00—Processes of treating or compounding macromolecular substances
    • C08J3/12—Powdering or granulating
    • C08J3/14—Powdering or granulating by precipitation from solutions
    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D5/00—Coating compositions, e.g. paints, varnishes or lacquers, characterised by their physical nature or the effects produced; Filling pastes
    • C09D5/03—Powdery paints

Definitions

  • This invention relates to a process for manufacturing thermosetting resin particles, particularly for powder coating use, having a narrow particle size distribution.
  • JP-A-58106554 can give linear or crosslinked vinyl polymer particles having a very narrow particle size distribution in which the weight average particle size nearly equals the number average particle size.
  • this method requires a number of steps for growing polymer particles stepwise making it unsuitable for a large scale industrial application.
  • it cannot be applied to the manufacture of polymer particles including foreign matters such as pigments.
  • JP-A-03200976 discloses a method for manufacturing colored or pigmented polymer particles in which monomers are polymerized in a dispersion in nonaqueous systems or solvent-water mixture systems. Because a large quantity of solvent is used, this method suffers from safety and environmental problems in handling, recovering or otherwise processing used solvents.
  • Powder coating compositions are generally produced by blending a binder resin with a crosslinker and optionally other additives such as pigments, kneading the mixture under heat to make a molten mass, pulverizing the mass and then classifying pulverized particles. The resulting particles are applied on a substrate using electrostatic spray coating, fluidized bed coating or other methods to form a film, and then baking the film.
  • powder coating compositions have certain defects. Since they tend to cause premature curing before use, chemicals or substances which react at a relatively low temperature cannot be added.
  • the weight average particle size of conventional powder coating compositions normally lie at around 30 ⁇ m, they are not satisfactory in terms of smoothness, luster and other aesthetic properties of finished films. Attempts have been made to produce finer particles having a weight average particle size of 10 ⁇ m or less by means of jet mills or other air stream mills. This approach is found effective to obtain much smoother and thinner films than the films of conventional powder coating compositions.
  • this powder coating composition comprises not only a large portion of microfine particles but also particles of irregular configuration. This makes the powder less free-flowing and increases the incidence of clogging of pneumatic conveyer pipes. Furthermore, it is conventional practice to recover and reuse excessively applied powder successively in the powder coating technology. If the proportion of microfine particles increases in the recovered powder, not only pneumatic transportation will become more difficult but also deposition efficiency of the powder onto the substrate will be greatly impaired.
  • thermosetting resin particles comprising the steps of:
  • This invention utilizes as its principle a surface chemical phenomenon in which a stable suspension of oil droplets in an aqueous solution of a water-soluble polymer having a cloud point becomes less stable when the suspension is heated to a temperature above the cloud point and the oil droplet particles therein grow up to larger secondary particles by agglomeration and fusing.
  • the suspension medium used in this invention also contains a water-soluble polymer not having such cloud point as a temperature-independent stabilizer.
  • Typical examples of water-soluble polymers having a cloud point within the range between 30°C and 90 °C include polyvinyl alcohol based polymers having a hydrophobic group or block such as partly saponified polyvinyl alcohol (partly saponified polyvinyl acetate) having a degree or saponification of not greater than 85 %, partly formalized polyvinyl alcohol or ethylene-vinyl acetate copolymer (saponified EVA); cellulose derivatives such as methylcellulose or hydroxypropylcellulose; and non-ionic surfactants such as polyethylene glycol monoalkyl ethers or ethylene oxide-propylene oxide block copolymers.
  • Water-soluble polymers not exhibiting cloud point themselves may be modified to have a cloud point within the above range by adding an amount of an electrolyte to their aqueous solutions. Two or more water-soluble polymers having a cloud point may be used in combination.
  • Typical examples of water-soluble polymers not having such cloud point include fully saponified polyvinyl alcohol, partly saponified polyvinyl alcohol having a degree of saponification of greater than 85 %, ethylcellulose, hydroxyethyl cellulose, polyethylene glycol and the like.
  • the weight ratio of the water-soluble polymer not having cloud point to the water-soluble polymer having cloud point may vary within a wide range depending upon the nature thereof and is generally from 99:1 to 10:90 to control the size of secondary particles in a suitable range.
  • the resin component from which particles are made according to this invention may be any resin which is thermocurable and also soluble or swellable in conventional organic solvents.
  • resins are well-known in the art and their selection is to be made depending upon the intended use of resin particles and properties requried therefor. Examples thereof includes polyesters, (meth)acrylate ester copolymers, aromatic vinyl compound copolymers, epoxy resins, phenol resins, melamine-formaldehyde resins, urea-formaldehyde resins and other thermosetting resins.
  • Resins which are not thermosetting themselves, such as polyester resins, (meth)acrylate ester copolymers or aromatic vinyl compound copolymers are combined with an external crosslinker. Polymers not soluble in a conventional solvent such as polyethylene or polypropylene may be incorporated into the resin particles by dispersing in a solvent-soluble resin compornent.
  • Any organic solvent which is substantially immiscible with water, namely having a solubility in water of less than 10 %, and has a boiling point of lower than 100 °C or is capable of forming an azeotropic mixture with water may be used in this invention. This is because the resin solution should be capable of forming oil droplets in water.
  • the resin component preferably consists of an epoxy, acrylic or polyester resin in combination with an appropriate crosslinker thereof.
  • crosslinkers include, as is well-known in the art, polycarboxylic anhydrides, dicyandiamide or acrylic resins for epoxy resins; polycarboxylic acids, epoxy resins or melamine resins for acrylic resins; and polycarboxylic acids and anhydrides, epoxy compounds, melamine resins or blocked polyisocyanates for polyester resins.
  • Particles for powder coating use may optionally contain various pigments such as titanium dioxide, ferric oxide, yellow iron oxide, carbon black, phthalocyanine blue or quinacridon red; surface conditioners such as polysiloxane or acrylic resins; plasticizers; UV absorbers; antioxidants; pigment dispersants; catalysts such as amines, imidazoles or cation polymerization initiators; and other resins. These additives may be dissolved or dispersed in the resin solution.
  • the liquid thermosetting resin composition containing an organic solvent is dispersed in an aqueous solution containing a water-soluble polymer having cloud point and a water-soluble polymer not having cloud point in step (b) at a temperature below said cloud point so that the mixture forms a suspension in which the liquid resion composition is suspended as primary particles of oil droplets having a number average particles size of less than 10 ⁇ m.
  • the proportions of the water-soluble polymer having cloud point and the water-soluble polymer not having cloud point may be varied, as stated before, depending upon the nature of particular liquid resin composition and the desired particle size.
  • the total concentration of the water-soluble polymers in the aqueous solution is preferably from 0.02 to 20 % by weight, and the ratio of the liquid resin composition to the aqueous solution is preferably from 1:0.5 to 1:3.
  • Mixing of these two components may be accomplished by means of a homogenizer when their viscosities are relatively low. When their viscosities are relatively high, mixing may be accomplished by means of a universal mixer or a planetary mixer.
  • the liquid resin composition and the aqueous solution do not initially form a suspension, the liquid resin composition is dispersed first in an aqueous solution solely containing the water-soluble polymer not having cloud point optionally in combination with a conventional surfactant to make a suspension. Thereafter the water-soluble polymer having cloud point may be added to the suspension.
  • the suspension is adjusted to a final resin composition concentration of from 10 to 50 % by weight by diluting, where necessary, with deionized water.
  • the suspension thus produced is heated in step (c) to a temperature higher than the cloud point.
  • This temperature depends on the cloud point of a particular water-soluble polymer and the nature of a particular liquid resin composition. A portion of the organic solvent contained in the liquid resin composition will be distilled off during the course of this heating or by subsequently heating the suspension to a temperature higher than the cloud point. Oil droplets initially formed as primary particles will normally agglomerate into secondary particles of large size as the temperature increases above the cloud point. In order to accomplish a desired particle size in the final particles, the growth of oil droplets may be terminated by distilling off remaining portions of the organic solvent to increase the viscoelasticity of the particles or cooling the suspension to a temperature below the cloud point. As stated before, this may also be done by selecting appropriate ratio of the water-soluble polymer not having cloud point to the water-soluble polymer having a cloud point.
  • the temperature at which the solvent is distilled off in step (d) may be easily controlled by applying vacuum or reduced pressure. Therefore, resin particles containing a component susceptible to a chemical reaction itself or with another component at a predetermined temperature, as in case of powder coating compositions, can be produced by using a water-soluble polymer having a cloud point substantially lower than the reaction temperature and distilling off the organic solvent at a temperature below the reaction temperature in vacuo.
  • the present invention thus enables to control oil droplets in the suspension to be of relatively uniform size.
  • the mechanism behind the formation of relatively uniform size of particles is postulated as follows.
  • the water-soluble polymer having a cloud point present as a stabilizer of oil droplets in the dispersion becomes less soluble in water and less effective to stabilize the suspension as the temperature increases above the cloud point.
  • the total surface area of dispersed phase decreases and finer particles tend to agglomerate with each other into larger secondary particles to accomodate the decrease in the total surface area of dispersed phase.
  • finer particles have larger specific surface areas than coarse particles, they will preferentially agglomerate into larger secondary particles. This contributes to a narrow particle size distribution of secondary particles even when starting from primary particles having wider particle size distributions.
  • the final particles may be recovered from the suspension by any conventional means such as filtering or centrifugation, and then dried.
  • the final particles thus obtained generally have a ratio of weight average particle size to number average particle size of less than 2.
  • the present invention can achieve other significant advantages.
  • the present invention enables the melting point and/or pigment dispersibility of the final particles to be easily adjustable. It also enables to modify the surfaces of particles to have various functional groups. Contrary to the prior art methods, it is possible to incorporate into the particles an additive which would adversely affect the polymerization reaction of monomers or use a varity of resins, crosslinkers and additives such as epoxy resins, acrylic resins, polyester resins, polycarboxylic acids, blocked polyisocyanate, pigments, surface conditioners or UV absorbers.
  • the resin particles produced by the present invention not only have a predetermined particle size but also consist mainly of spherical particles with lesser proportions of microfine and irregular shape particles than particles produced by the prior art methods, they are free-flowing and produce a thin coating film having excellent appearance properties.
  • the present invention can also be applied to the manufacture of particles of thermoplastic resins.
  • the present invention could be applied to the production of toners for electrophotography by mixing a thermoplastic resin such as styrene/acrylic or polyester resins with a pigment such as carbon black and a electrostatic charge controlling agent such as azo- or nigrosine dyes.
  • the mixture was heated to 190°C and then to 240°C over 3 hours while removing water.
  • the condensation reaction was then continueded until an acid number of 5 was reached.
  • the product was cooled to 100°C and dissolved in 100 parts of xylene.
  • thermosetting resin composition was produced by mixing the following materials in a sand grind mill.
  • an aqueous solution was prepared by dissolving 6 parts of GOHSENOL GH-20 (polyvinyl alcohol having a degree of saponification of 88 % sold by The Nippon Synthetic Chemical Industry Co., Ltd.) and 4 parts of GOHSENOL KL-05 ( polyvinyl alcohol having a degree of saponification of 80 % sold by The Nippon Synthetic Chemical Industry Co., Ltd.) in 90 parts of deionized water.
  • GOHSENOL GH-20 polyvinyl alcohol having a degree of saponification of 88 % sold by The Nippon Synthetic Chemical Industry Co., Ltd.
  • GOHSENOL KL-05 polyvinyl alcohol having a degree of saponification of 80 % sold by The Nippon Synthetic Chemical Industry Co., Ltd.
  • the above resin composition and the aqueous solution were mixed in a homogenizer at 10 4 r.p.m. to make a suspension.
  • the particle sizes of suspended droplets were determined using a Coulter counter.
  • the weight average particle size was 4.6 ⁇ m and the number average particle size was 2.1 ⁇ m.
  • the suspension was then diluted with 300 parts of deionized water and placed in a container equipped with a stirrer, temperature control means, reflux condenser and pressure reducing means. Then the suspension was heated to 70 °C under a reduced pressure of 160 Torr (0,21 bar) until the solvent in the dispersed phase was completely removed and cooled to room temperature.
  • the resin particles thus produced were recovered by centrifugation, dried and tested for their particle size using a Coulter counter.
  • the weight average particle size was 8.6 ⁇ m and the number average particle size was 6.2 ⁇ m. Thus, the particle size distribution curve was very sharp.
  • Example 1 was followed except that the aqueous water-soluble polymer solution was replaced with a solution of 10 parts of GOHSENOL GH-20 and 2 parts of METOLOSE 65SH (methyl cellulose sold by Shin-Etsu Chemical Co., Ltd.) in 82 parts of deionized water.
  • the weight average particle size and the number average particle size of oil droplets in the resulting suspension were 5.1 ⁇ m and 2.3 ⁇ m, respsectively.
  • the suspension was then diluted with 300 parts of deionized water and placed in a container equipped with a stirrer, temperature control means, reflux condense and pressure reducing means. After removing about 90 % of the solvent contained in the dispersed phase by applying a reduced pressure of 20 Torr (0,026 bar), the remaining solvent was completely removed by heating the suspension to 70 °C at a reduced pressure of 160 Torr (0,21 bar). After cooling, the suspension was centrifuged and the separated particles were dried. The resin particles were found to possess a weight average particle size of 8.0 ⁇ m and a number average particle sise of 6.8 ⁇ m, exhibiting a sharp particle size distribution curve.
  • Example 1 was followed except that the aqueous water-soluble polymer solution was replaced with a solution of 10 parts of GOHSENOL GH-20 and 0.5 parts of METOLOSE 65SH in 82 parts of deionized water.
  • the weight average particle size and the number average particle size of oil droplets in the suspension were 4.7 ⁇ m and 2.2 ⁇ m, respectively.
  • the suspension was diluted with 300 parts of deionized water and then placed in the same container as used in the preceding Examples. After removing about 90 % of the solvent from the dispersed phase by applying a reduced pressure of 20 Torr (0,026 bar), the remaining solvent was completely removed by heating the suspension to 70°C at a reduced pressure of 160 Torr (0,21 bar). After cooling, the suspension was centrifuged and the separated particles were dried. The resin particles were found to possess a weight average particle size of 8.6 ⁇ m and a number average particle size of 4.4 ⁇ m, exhibiting a sharp particle size distribution curve.
  • Example 1 was followed except that the aqueous water-soluble polymer solution was replaced with a solution of 10 parts of GOHSENOL GH-20 in 82 parts of deionized water.
  • the weight average particle size and the number average particle size of oil droplets in the suspension were 8.6 ⁇ m and 3.3 ⁇ m, respectively.
  • the suspension was diluted with 300 parts of deionized water and then placed in the same container as used in the preceding Examples. After removing about 90 % of the solvent from the dispersed phase by applying a reduced pressure of 20 Torr (0,026 bar), the remaining solvent was completely removed by heating the suspension to 70°C at a reduced pressure of 160 Torr (0,21 bar). After cooling, the suspension was centrifuged and the separated particles were dried.
  • the powder coating composition thus produced were found to possess a weight average particle size of 8.9 ⁇ m and a number average particle size of 3.4 ⁇ m, exhibiting a broad particle size distribution curve. Most of particles were of sizes of oil droplets initially formed as primary particles.
  • thermosetting resin composition was produced by mixing the following materials in a sand grind mill.
  • Material Parts Resin solution B 80 Epoxy resin (EPOTOHTO YD-014 sold by Toto Kasei K.K.) 5 Methyl isobutyl ketone 10 Curing agent (blocked polyisocyanate) 10 Benzoin 0.3 Polysiloxane surface conditioner 0.1 Titanium dioxide 20 Total 100
  • a water-soluble polymer solution was produced by dissolving 4 parts of GOHSENOL GH-20 and 3 parts of GOHSENOL KL-05 in 93 parts of deionized water.
  • the above resin composition and the aqueous solution were mixed in a planetary mixer to obtain a suspension of oil droplets having a weight average particle size of 4.2 ⁇ m and a number average particle size of 2.0 ⁇ m.
  • the suspension was then diluted with 250 parts of deionized water and 50 parts of a 5 % aqueous solution of hydroxypropyl cellulose, and then placed in the same container as used in the preceding Examples. After removing about 90 % of the solvent from the dispersed phase by applying a reduced pressure of 20 Torr (0,026 bar), the remaining solvent was completely removed by heating the suspension to 70°C at a reduced pressure of 160 Torr (0,21 bar). After cooling, the suspension was centrifuged and the separated particles were dired. The particles were found to possess a weight average particle size of 9.6 ⁇ m and a number average particle size of 7.1 ⁇ m, exhibiting a sharp particle size distribution curve.
  • Example 4 was followed except that the aqueous solution was replaced with a solution containing 2 parts of GOHSENOL GH-20 and 8 parts of GOHSENOL KL-05 in 93 parts of deionized water. A suspension of oil droplets having a weight average particle size of 4.5 ⁇ m and a number average particle size of 2.1 ⁇ m was obtained.
  • the suspension was diluted with 250 parts of deionized water and 50 parts of a 5 % aqueous solution of hydroxypropyl cellulose, and placed in a container as used in the preceding Examples. After removing about 90 % of the solvent contained in the dispersed phase by applying a reduced prressure of 20 Torr (0,026 bar), the remaining solvent was completely removed by heating the suspention to 70°C at a reduced pressure of 160 Torr (0,21 bar). After cooling, the suspension was centrifuged and the separated particles were dried. The particles thus produced were found to possess a weight average particle size of 15.3 ⁇ m and a number average particle size of 7.9 ⁇ m, exhibiting a sharp particle size distribution curve.
  • Example 4 was followed except that the aqueous solution was replaced with a solution of 10 parts of GOHSENOL GH-20 in 82 parts of deionized water to produce a suspension of oil droplets having a weight average particle size of 10.9 ⁇ m and a number average particle size of 3.2 ⁇ m.
  • the suspension was diluted with 300 parts of deionized water and placed in the container as used in the preceding Examples. After removing about 90 % of the solvent contained in the dispersed phase by applying a reduced pressure of 20 Torr (0,026 bar), the remaining solvent was completely removed by heating the suspension to 70°C at a reduced pressure of 160 Torr (0,21 bar). After cooling, the suspension was centrifuged and the separated particles were dried. The particles thus produced were found to possess a weight average particle size of 11.3 ⁇ m and a number average particle size of 3.2 ⁇ m, exhibiting a wide particle size distribution curve. Most of particles were of sizes of oil droplets initially formed as primary particles.
  • Example 4 was followed except that the aqueous solution was replaced with a solution containing 8 parts of GOHSENOL KL-05 and 2 parts of METOLOSE 65SH in 82 parts of water. A suspension of oil droplets having a weight average particle size of 4.2 ⁇ m and a number average particle size of 1.7 ⁇ m was obtained.
  • the suspension After diluting with 300 parts of deionized water, the suspension was placed in the same container as used the preceding Examples. After removing about 90 % of the solvent contained in the dispersed phase by applying a reduced pressure of 20 Torr (0,026 bar), the remaining solvent was completely removed by heating the suspension to 70°C at a reduced pressure of 20 Torr (0,026 bar). The product contained a large amount of cakes or coarse particles, making it unusable for powder coating.
  • Example 1-5 and Comparative Examples 1-2 were tested for their performance. Each composition was applied electrostatically on a steel plate and baked at 160°C for 30 minutes to produce a cured film of 50 ⁇ m film thickness. The appearance was evaluated in terms of NSIC (%) measured by a reflected image distinctiveness meter (Suga Testing Instrument Co., Ltd.).
  • Applicator systems used in the powder coating technology normally comprise a powder feeder (fluidized bed), injector, conveying hose and spray gun. Workability of powders of Examples and Comparative Examples was evaluated by operating the above applicator for 1 hour continuously with each powder, and judged based on the volume of powder accumlated in the injector and the hose according to the following schedule.

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  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Polymers & Plastics (AREA)
  • Medicinal Chemistry (AREA)
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Claims (12)

  1. Procédé de fabrication de particules de résine thermodurcissables comprenant les étapes consistant à :
    (a) apporter un premier polymère hydrosoluble ayant un point de rosée compris entre 30°C et 90°C et un second polymère hydrosoluble n'ayant pas de point de rosée;
    (b) préparer une suspension aqueuse d'une composition de résine liquide thermodurcissable contenant un solvant organique, ayant une température inférieure au point de rosée dudit premier polymère hydrosoluble, dans laquelle ladite composition de résine est suspendue sous forme de particules primaires de gouttelettes d'huile ayant une taille de particule moyenne inférieure à 10 microns dans un milieu de suspension aqueux contenant lesdits premier et second polymères hydrosolubles;
    (c) chauffer ladite suspension à une température supérieure au dit point de rosée pour permettre auxdites particules primaires de s'agglomérer et de fusionner en particules secondaires ayant une taille de particule moyenne de 2 à 20 fois supérieure à celle des particules primaires; et
    (d) distiller le solvant desdites particules secondaires durant ou après l'étape (c).
  2. Procédé selon la revendication 1 comprenant en outre l'étape de récupération desdites particules secondaires dans de la suspension.
  3. Procédé selon la revendication 1 dans lequel le rapport entre ledit polymère ayant un point de rosée et ledit polymère n'ayant pas de point de rosée est compris entre 1:99 et 90:10 en poids.
  4. Procédé selon la revendication 1 dans lequel ledit polymère hydrosoluble ayant un point de rosée est choisi parmi un alcool polyvinylique ayant un degré de saponification inférieur à 85 %, des alcools polyvinyliques partiellement formalisés, des copolymères d'alcool vinylique et d'éthylène, la méthyl cellulose, l'hydroxypropyl cellulose, les éthers monoalkyliques de polyalkylène glycol, ou les copolymères bloc d'oxyde de propylène et d'oxyde d'éthylène.
  5. Procédé selon la revendication 1 dans lequel ledit polymère hydrosoluble n'ayant pas de point de rosée est choisi parmi les alcools polyvinyliques ayant un degré de saponification supérieur à 85 %, l'éthyl cellulose, l'hydroxyéthyl cellulose ou les polyéthylène glycols.
  6. Procédé selon la revendication 1 dans lequel ledit solvant organique a un point d'ébullition inférieur à 100°C ou peut être éliminé par distillation azéotropique avec de l'eau.
  7. Procédé selon la revendication 1 dans lequel la concentration desdits premier et second polymères hydrosolubles dans ledit milieu de suspension aqueux est comprise entre 0,02 et 20 % en poids.
  8. Procédé selon la revendication 1 dans lequel la concentration finale en ladite composition de résine thermodurcissable liquide dans ladite suspension est comprise entre 10 et 50 % en poids.
  9. Procédé selon la revendication 1 dans lequel ladite composition de résine thermodurcissable liquide comprend une résine liante et un agent de réticulation.
  10. Procédé selon la revendication 9 dans lequel ladite résine liante est une résine époxy, acrylique ou polyester.
  11. Composition de revêtement en poudre comprenant les particules de résine thermodurcissables obtenues par le procédé de la revendication 9.
  12. Composition de revêtement en poudre comprenant les particules de résine thermodurcissables obtenues par le procédé de la revendication 10.
EP95119961A 1995-10-03 1995-12-18 Procédé pour la fabrication de particules de résine thermodurcissables Expired - Lifetime EP0768333B1 (fr)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP27973495 1995-10-03
JP27973495A JP3543201B2 (ja) 1995-10-03 1995-10-03 熱硬化性樹脂粒子の製造方法
JP279734/95 1995-10-03

Publications (3)

Publication Number Publication Date
EP0768333A2 EP0768333A2 (fr) 1997-04-16
EP0768333A3 EP0768333A3 (fr) 1997-07-30
EP0768333B1 true EP0768333B1 (fr) 1999-09-08

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EP95119961A Expired - Lifetime EP0768333B1 (fr) 1995-10-03 1995-12-18 Procédé pour la fabrication de particules de résine thermodurcissables

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US (1) US5610269A (fr)
EP (1) EP0768333B1 (fr)
JP (1) JP3543201B2 (fr)
KR (1) KR100243706B1 (fr)
CN (1) CN1063452C (fr)
CA (1) CA2165878C (fr)
DE (1) DE69512070T2 (fr)
TW (1) TW324726B (fr)

Families Citing this family (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH10130541A (ja) * 1996-10-29 1998-05-19 Nippon Paint Co Ltd 粉体塗料およびその製造方法
WO1999023534A1 (fr) * 1997-10-31 1999-05-14 Sanyo Chemical Industries, Ltd. Toner et liant pour toner
US6506820B2 (en) * 1998-04-16 2003-01-14 Nippon Paint Co., Ltd. Method for manufacture of particles for powder coating
JPH11343432A (ja) * 1998-06-02 1999-12-14 Dainippon Toryo Co Ltd 水性分散塗料の製造方法及び粉体塗料の製造方法
US6313221B1 (en) * 1999-05-28 2001-11-06 Nippon Paint Co., Ltd. Powder coating of epoxy-acrylic resin, polycarboxylic acid, crosslinked particles and liquid resin
JP2001064574A (ja) * 1999-08-31 2001-03-13 Nippon Paint Co Ltd 熱硬化性粉体塗料組成物
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DE69512070T2 (de) 2000-05-31
CN1063452C (zh) 2001-03-21
US5610269A (en) 1997-03-11
CA2165878C (fr) 2001-10-23
CN1147000A (zh) 1997-04-09
EP0768333A2 (fr) 1997-04-16
KR970022594A (ko) 1997-05-30
KR100243706B1 (ko) 2000-02-01
TW324726B (en) 1998-01-11
JP3543201B2 (ja) 2004-07-14
DE69512070D1 (de) 1999-10-14
JPH09100414A (ja) 1997-04-15
EP0768333A3 (fr) 1997-07-30
CA2165878A1 (fr) 1997-04-04

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